CN110799797B

CN110799797B - Furnace with a heat exchanger

Info

Publication number: CN110799797B
Application number: CN201880040545.1A
Authority: CN
Inventors: M·穆克; D·萨贝尔费尔德
Original assignee: Onejoon GmbH
Current assignee: Onejoon GmbH
Priority date: 2017-06-19
Filing date: 2018-06-13
Publication date: 2023-03-31
Anticipated expiration: 2038-06-13
Also published as: DE102017113342A1; EP3735564B1; US20200181809A1; WO2018234126A1; KR102552048B1; US11603607B2; EP3735564A1; ES2967442T3; CN110799797A; KR20200019883A

Abstract

Furnace (10) for the thermal treatment of materials, in particular for carbonization and/or graphitization of materials, in particular fibers (12), in particular fibers (14) formed from oxidized Polyacrylonitrile (PAN), wherein pyrolysis gases are released from the materials during the thermal treatment. The furnace (10) comprises: a housing (16); a process chamber (22) located in the interior (18) of the housing (16), which is delimited by a process chamber housing (24) and through which material can be conducted; a heating system (32) by means of which a process chamber gas (30) filled in the process chamber (22) can be heated; and an exhaust system (48) by means of which the process chamber gas (30) carrying the pyrolysis gas can be sucked out of the process chamber (22). The exhaust system (48) comprises at least one suction device (52) having a suction channel (60) delimited by a channel wall (58) and connected to the process chamber (22) via a suction opening (62). The suction opening (62) is arranged in a region (68) of the process chamber (22) in which, during operation of the furnace (10), a temperature exists at which no chemical reaction or only a moderated chemical reaction takes place between the pyrolysis gas and the process chamber housing (24) and/or the channel wall (58).

Description

Furnace with a heat exchanger

Technical Field

The invention relates to a furnace for the thermal treatment of materials, in particular for carbonizing and/or graphitizing materials, in particular fibers made of oxidized Polyacrylonitrile (PAN), wherein pyrolysis gases are released from the materials during the thermal treatment, comprising:

a) A housing;

b) A process chamber located in the inner chamber of the housing, which process chamber is delimited by the process chamber housing and through which process chamber material can be guided;

c) A heating system by means of which a process chamber gas/atmosphere in the process chamber can be heated;

d) An exhaust system by means of which the process chamber gases carrying the pyrolysis gases can be drawn out of the process chamber.

Background

Such furnaces are used in particular for the production of carbon fibres which are formed in a three-stage or four-stage process from fibres comprising polyacrylonitrile-fibres. Polyacrylonitrile is hereinafter mostly abbreviated as PAN. Felts and nonwovens can also be treated in such ovens. Other materials as PAN are for example viscose and lignin.

In the first production stage, polyacrylonitrile is oxidized in the presence of oxygen in an oxidation oven at a temperature between about 200 ℃ and 400 ℃ to form oxidized PAN fibers.

This oxidized PAN fiber is subsequently subjected to a heat treatment in a second production stage in a furnace at approximately 400 ℃ to 1000 ℃ in an inert gas atmosphere free of oxygen, in order to increase the carbon content of the fiber by carbonization, which is approximately 62% by weight in the oxidized PAN fiber. Nitrogen gas N is generally used ₂ Or argon as an inert gas.

In a third production phase, the heat treatment is carried out in a furnace of the type mentioned at the outset, referred to as high-temperature furnace, at temperatures between 800 ℃ and 1800 ℃ under a nitrogen atmosphere, wherein carbonization is carried out in which the PAN fibers are cracked until the fibers have a carbon content of approximately 92 to 95% by weight.

If necessary, the carbon fibers obtained after the third production phase are subjected to a further heat treatment in a fourth production phase in a furnace of the type mentioned at the outset at a temperature of between 1800 ℃ and 3000 ℃ in an inert gas atmosphere which is free of oxygen; graphitization of the carbon fibers, which subsequently have a carbon fraction of more than 99 weight percent and are referred to as so-called graphite fibers, is carried out at such temperatures. Argon is generally used as an inert gas in graphitization.

If the oxidized PAN fiber is heat-treated at temperatures above 700 ℃ in an inert gas atmosphere free of oxygen, a pyrolysis gas is released from the PAN fiber, which also contains hydrocyanic acid HCN, nitrogen N2, ammonia NH3, carbon dioxide CO2, carbon monoxide CO and methane CH4. Since the hydrocyanic acid HCN contained is particularly highly toxic, the process chamber gas loaded with the pyrolysis gas is drawn off from the process chamber by means of an exhaust system and conveyed to a downstream purification unit. The process gas atmosphere sucked out and loaded with the pyrolysis gas is burned in most cases, but facilities also exist in which hydrocyanic acid is chemically converted in order to obtain hydrocyanic acid as a material resource.

The process chamber is lined in the known high-temperature furnace with a muffle/muffle furnace with a material which reacts chemically with and is attacked by the pyrolysis gas released from the PAN-fibres. Among the furnaces known from the market are muffle furnaces made of graphite, which are attacked by the cracking gas at temperatures above about 1000 ℃. The exhaust gas duct or exhaust gas line of the exhaust system, through which the process chamber gases carrying the pyrolysis gases are conducted away from the process chamber, is also usually lined with muffle material; the exhaust gas duct or exhaust gas line therefore reacts at the respective temperature with the process gas being drawn off and carrying the pyrolysis gas and is attacked. Over time, damage occurs in the muffle and in the exhaust gas duct or exhaust gas line as a result of the pyrolysis gas.

The following methods exist: the muffle itself is additionally covered with so-called sacrificial graphite plates in the process chamber, which are subsequently replaced at regular intervals. However, there is still a problem in the exhaust gas passage.

Disclosure of Invention

The object of the invention is to provide a furnace of the type mentioned in the introduction, in which the load on the process chamber and the load on the channels or pipes through which the process gas carrying the pyrolysis gas is conducted are reduced.

The object is achieved by:

e) The exhaust system comprises at least one suction device having a suction channel delimited by channel walls, which suction channel is connected to the process chamber via a suction opening;

f) The suction opening is arranged in the region of the process chamber, in which region during operation of the furnace a temperature exists at which no chemical reaction or only a moderate/controlled chemical reaction between the pyrolysis gas and the process chamber housing and/or the channel wall takes place.

The invention is based on the recognition that the load on components and parts which come into contact with the pyrolysis gas and react in an undesired manner with the pyrolysis gas can be significantly reduced if it is ensured that the pyrolysis gas is sucked off in an early stage of the heat treatment at a temperature at which no reaction of the participating parts takes place. For this purpose, the suction point defined by the position of the suction opening of the suction channel is specifically arranged in a region of the process chamber, in which a correspondingly low temperature prevails.

Preferably, a temperature of less than 1000 ℃, preferably less than 900 ℃, particularly preferably less than 800 ℃ is present in the region during operation of the furnace.

Advantageously, the region is located next to or in the vicinity of the inlet opening of the process chamber housing for the material to be treated. In this way, the following can be advantageously exploited: the temperature in the process chamber generally rises gradually from the inlet to the outlet, and in any case in the region after the inlet there may be a temperature at which no undesired reactions occur. At the beginning of the process chamber, usually already a maximum fraction of the pyrolysis gas is released from the fibers, which is effectively removed in this way without causing greater damage. The amount of pyrolysis gas released at higher temperatures in the subsequent regions of the process chamber is in a reasonable manner negligible by comparison.

A structure that can be realized technically with relatively little effort is realized by: the suction channel extends through the inlet opening into the process chamber.

In different operating modes of the same furnace, it can happen that the zones filled with the desired, relatively low temperature are formed at different points in the process chamber. It is therefore advantageous if the suction channel is designed such that the position of the suction opening is variable.

Preferably, the suction channel further comprises a plurality of channel sections, which are detachably connected to one another, so that the length of the suction channel can be adjusted by the number of channel sections provided. The suction channel can thus be lengthened or shortened in a modular manner.

Advantageously, the suction channel is connected at the end remote from the suction opening to a collecting channel, which is itself connected to the hot post-combustion device. If there are a plurality of suction channels, the plurality of suction channels can be collected in a common collection channel or connected to one collection channel per se.

Advantageously, a passage jacket (Durchgangs-Einhausung) of the suction device is arranged upstream of the inlet passage of the housing, in which passage jacket the collecting channel extends at least partially. Such an enclosure can be arranged in a simple manner between the housing of the furnace and the mostly existing entry lock and is therefore integrated in the overall system.

The aspiration system can be used particularly well if the process chamber housing is designed as a muffle, in particular as a muffle made of graphite.

The aspiration system works particularly effectively even if the aspiration channel and/or the collection channel are made of graphite or lined with graphite.

Drawings

The present invention is described in detail below with reference to the accompanying drawings. The figures show that:

fig. 1 shows a perspective view of a furnace for the thermal treatment of carbon fibres, having an exhaust system for the production gas atmosphere, comprising suction means;

fig. 2 shows a perspective view of the suction device with the housing broken away, so that a suction channel can be identified, which extends through the inlet into the process chamber;

FIG. 3 shows a partial section through the furnace, in which one of the suction channels of the suction device, which is connected to the process chamber via the suction opening, can be identified;

FIG. 4 shows a partial section of the furnace, in which the position of the suction mouth of the suction channel is changed with respect to that in FIG. 3;

FIG. 5 shows a partial section through the furnace, in which the position of the suction openings of the suction channel again changes with respect to the position in FIGS. 3 and 4;

FIG. 6 shows a partial section of the furnace, in which the suction channels are shown in a modified arrangement;

FIG. 7 shows a partial section of the furnace, in which two suction channels can be identified;

figure 8 shows a perspective view of the suction device, including a sectioned housing of a variant of the suction device;

figure 9 shows a perspective view of the suction device, including a sectioned housing of another variant of the suction device;

figure 10 shows a partial cross section of a modified oven.

Detailed Description

In the figure, a furnace 10 is shown for the thermal treatment of a material, which in the exemplary embodiment shown in fig. 1 to 9 is a fiber 12, for example a fiber 14 made of oxidized polyacrylonitrile, which is referred to below as oxPAN fiber 14.

The furnace 10 includes a thermally insulated furnace housing 16 that defines an internal chamber 18. The furnace housing 16 has a fiber inlet passage 20 on one end face and a fiber outlet passage on the opposite end face, which is not shown in the drawing for reasons of perspective.

In the inner chamber 18 of the furnace housing 16, a process chamber 22 is provided, which is in turn delimited by a process chamber housing 24 in the form of a muffle 26. In the present embodiment, the muffle 26 is made of graphite. The process chamber housing 24, that is to say the muffle 26, has a fiber inlet opening 28 on one end face and a fiber outlet opening on the opposite end face, which is likewise not shown in the drawing. During operation of the furnace 10, the process chamber 22 is filled with process chamber gas 30.

The furnace 10 includes a heating system 32 with which the process chamber gas 30 is heated. In this case, a continuous heating zone 34 is formed in the process chamber 22 between the fiber inlet opening 22 and the fiber outlet opening of the muffle 26, in which five heating zones 34.1, 34.2, 34.3, 34.4 and 34.5 can be seen in fig. 1. The temperature increases from the heating zone to the further heating zone in such a way that a temperature gradient of about 800 ℃ to about 1800 ℃ exists in the process chamber 22. Each heating zone 34 is provided with a dedicated heating device 36, which heats the muffle 26 in the respective heating zone 34, as is known per se. For this purpose, the muffle 26 is surrounded in each heating zone 34, for example, by a heating housing, not shown in particular, which is arranged in the space between the muffle 26 and the furnace housing 16. The space defines a heating chamber 38 that surrounds the muffle 26.

The heating chamber 38 is delimited at the end by an insulating element 39, which is schematically shown only by lines. The heating chamber 38 is filled with an inert gas atmosphere, for which purpose the heating chamber is fed with inert gas by means of an inert gas device not shown in particular; nitrogen gas is usually mixed with ₂ As an inert gas for heating chamber 38.

On the inlet side, the furnace 10 comprises: an inlet shutter 40 having a separate shutter housing 42; and an outlet lock, which is also not shown in the illustrated view due to the angle of view, and which has a separate lock housing. The heat treatment of the oxPAN fibers 14 is carried out in an inert gas atmosphere by supplying an inert gas 46 through the inlet lock 40 into the inner chamber 18 of the furnace housing 16 and thus into the heating chamber 38 and the process chamber 22 by means of an inert gas device 44. As mentioned at the outset, nitrogen gas N is used in practice ₂ Or argon gas is used as the inert gas. The process chamber gas 30 is thus a cracked gas released from the inert gas and during the treatment of the oxPAN-fibers 14A mixture of gases.

The furnace 10 also includes an exhaust system, generally indicated at 48, by which the process chamber gases 30 can be drawn from the process chamber 22.

In the present exemplary embodiment, a passage jacket 50 of a suction device 52 of the exhaust system 48 is arranged between the inlet lock 40 and the furnace housing 16, which passage jacket delimits a flow chamber 54. The flow chamber 54 is connected on one side in a gas-tight manner to the inlet lock 40 and on the other side in a gas-tight manner to the furnace housing 16, so that the inert gas 46 can flow from the inlet lock 40 through the flow chamber 54 into the process chamber 22.

The oxPAN fibers 14 are guided by means of a not specifically illustrated, per se known conveying system as a fiber blanket 56 through the inlet sluice 40, through the flow chamber 54 and further through the fiber inlet passage 20 of the furnace housing 16 into its inner chamber 18 and there through the fiber inlet opening 26 of the process chamber housing 24 into the process chamber 22. Fiber blanket 56 is guided out of furnace 10 through process chamber 22 and heating zone 34 located there and thereafter through the fiber outlet opening of process chamber housing 24 and through the fiber outlet passage of furnace housing 16 and finally through the outlet sluice connected thereto.

In order to now suck out the process chamber gas 30 loaded with the pyrolysis gas, the suction device comprises at least one suction channel 60, which is delimited by a channel wall 58 and is connected to the process chamber 22 via a suction opening 62. In the embodiment shown, there are two such suction channels 60, which carry the same reference numerals; in principle, only one suction channel 60 is sufficient. The suction channel 60 is made of graphite or lined with graphite as is the muffle 26.

In the present exemplary embodiment, a suction opening 63, which is complementary to the variant, is provided in duct wall 58 on the side facing fiber blanket 56; however, in most cases such suction ports 63 may be omitted.

The suction channel 60 has a suction opening 62 at its free end and is connected at its end remote from the suction opening 62 in the flow chamber 54 of the suction device 52 to a collecting channel 64 which extends through the passage casing 50 on both sides outwards and is guided there to in each case one hot post-combustion device 66. The collection channel 64 is also made of graphite or lined with graphite.

Other components, parts and exhaust gas channels or exhaust gas ducts of the exhaust system 48, through which the generated exhaust gases are output from the hot post-combustion device 66, are not particularly shown for reasons of simplicity.

A suction channel 60 extends from the flow chamber 54 of the suction device 52 through the fiber inlet passage 20 of the furnace housing 16 and through the fiber inlet opening 28 of the muffle 26 into the process chamber 22, wherein the suction channel 60 is arranged above the fiber blanket 56.

The suction opening 62 of the suction channel 60 is located in the process chamber 22 in such a way that it is positioned in a region of the process chamber 22 which defines an inert gas suction region and in which there is a temperature at which no chemical reaction or at least only a moderate/controlled chemical reaction takes place between the pyrolysis gas in the process chamber gas 30 and the muffle 26 and the suction channel 60. The cracked gas is prevented or reduced from chemically reacting with collection channel 64 and other, not shown, conduits of exhaust system 48. With regard to the graphite as material for the muffle 26 and the suction channel 60, the temperature in the region is not allowed to be higher than approximately 1000 ℃, since at this temperature an undesired chemical reaction takes place between the graphite and the pyrolysis gas.

In practice it is noted that there are temperatures in the zone below 900 c, more preferably below 800 c. The region is most often placed directly next to the fiber inlet opening 28 of the process chamber 22.

Depending on the operating mode of the furnace 10, the position of the region within the process chamber 22, which is defined by the temperature prevailing there, can, however, also be varied or the length of the region can be varied, on the basis of the adjusted temperature profile in the process chamber 22. Thus, the suction channel 60 is designed such that the position of the suction opening 62 can be changed.

In the present exemplary embodiment, for this purpose, the suction channel 60 is composed of channel sections 72 in an end section 70 comprising the suction opening 62, which are detachably connected to one another, so that the length of the suction channel 60 can be adjusted by the number of channel sections 72 provided.

Fig. 3 shows an end section 70 which is composed of three channel sections 72. Fig. 4 shows a suction channel 60, the end section 70 of which is formed by four channel sections 72, so that the suction opening 62 is arranged further from the fiber inlet opening 28 and further inside the process chamber 22 than in fig. 3. Fig. 5 shows a suction channel 60, the end section 70 of which consists of only two channel sections 72, so that the suction opening 62 is arranged closer to the fiber inlet opening 28 and thus closer to the inside of the process chamber 22 than in fig. 3 and 4.

The channel sections 72, which are respectively located at the ends, thus respectively define the suction openings 62 of the suction channel 60. If additional suction openings 63 are provided, they are correspondingly located in the channel section 72.

In a variant that is not shown in particular, the suction channel 60 can also be designed to be variable in terms of its shape, so that the position of the suction opening 62 can be shifted in such a way that the curve of the suction channel 60 changes and the suction channel can be designed, for example, in an arc shape.

Fig. 6 shows a modified suction device 52 in which a suction channel 60 is arranged below the fibre blanket 56. The above applies in other respects.

Fig. 7 shows a further modified suction device 52. Where one suction channel 52 extends above fiber blanket 56 and one suction channel 52 extends below the fiber blanket. On the other hand, suction channel 52 does not have a suction opening at its free end, but rather has a plurality of lateral suction openings 62, which may be understood as suction openings 62 that are arranged laterally in channel wall 58 on the side wall and/or on the side pointing toward fiber blanket 56.

If the suction channel 60 can be varied in its length by means of the respective channel section 70, as in the previous exemplary embodiment, a suction opening is provided at the free end of the suction channel 60. The channel section 70 can then have a corresponding lateral suction opening 62 in the channel wall 58.

Fig. 8 shows a variant in which each of the two suction channels 60 is connected to its own collecting channel 64, which in each case lead to its own hot post-combustion device, which is not shown separately again in fig. 8.

Fig. 9 shows a variant in which two further existing suction channels 60 are connected to a common collecting channel 64; however, the collecting channel passes through the passage casing 50 of the suction device 52 on only one side.

Fig. 10 shows a variant of a furnace 10 which is not used for the heat treatment of the fibers 12, but rather for the heat treatment of the plate-shaped material 74, in which pyrolysis gases are released. Such materials include, for example, hard felt. Continuous materials as rolls, such as non-woven fabrics and soft felts, can also be included in the sheet material.

Such sheet-shaped material 74 is conveyed through the process chamber 22 by means of a conveying device, which is not shown in particular, and which may be, for example, a propulsion system. In the variant shown in fig. 10, the suction channel 60, of which only one can be seen for reasons of section, extends above the material 74 and in turn has lateral suction openings on the side walls and the side of the channel wall 58 directed toward the material 74. Furthermore, the collecting channel 64 in this variant does not extend laterally, but rather upwards through the passage shell 50 of the suction device 52.

In a variant of the exemplary embodiment described above, which is not illustrated in particular, the suction channel 60 can additionally be designed with a protective plate made of silicon carbide SiC. If a temperature is to be reached at the suction opening 62, at which a chemical reaction of the pyrolysis gas with the muffle 26 or the suction channel 60 can take place, the SiC is reduced chemically, wherein the muffle 26 remains protected.

Claims

1. A furnace for the thermal treatment of materials, wherein a pyrolysis gas is released from the materials during thermal treatment, the furnace comprising:

a) A housing (16);

b) A process chamber (22) located in the interior (18) of the housing (16), which process chamber is delimited by a process chamber housing (24) and through which the material can be conducted, the process chamber housing (24) having an inlet opening (28) for the material to be treated;

c) A heating system (32) by means of which the process chamber gas (30) in the process chamber (22) can be heated;

d) An exhaust system (48) by means of which the process chamber gas (30) carrying the pyrolysis gas can be sucked out of the process chamber (22),

it is characterized in that the preparation method is characterized in that,

e) The exhaust system (48) comprises at least one suction device (52) having a suction channel (60) which is delimited by a channel wall (58) and which is connected to the process chamber (22) via a suction opening (62), wherein the suction channel (60) extends through the inlet opening (28) into the process chamber (22);

f) The suction opening (62) is arranged in a region of the process chamber (22) which is located next to or in the vicinity of the inlet opening (28) of the process chamber housing (24) for the material to be treated, in which region a temperature exists during operation of the furnace (10) at which no chemical reaction or only a moderated chemical reaction takes place between the cracking gas and the process chamber housing (24) and/or the channel wall (58).

2. The furnace according to claim 1, characterized in that in operation of the furnace (10) there is a temperature in said zone lower than 1000 ℃.

3. The furnace according to claim 1, characterized in that the suction channel (60) is arranged such that the position of the suction opening (62) is changeable.

4. The furnace according to claim 3, characterized in that the suction channel (60) comprises a plurality of channel sections (72) which are releasably connected to each other, so that the length of the suction channel (60) can be adjusted by the number of channel sections (72) provided.

5. The furnace according to any of the claims 1 to 4, characterized in that the suction channel (60) is connected on the end remote from the suction opening (62) with a collecting channel (64) which is itself connected with a hot post-combustion device (66).

6. The furnace according to claim 5, characterized in that a passage envelope (50) of a suction device (52) is arranged before the entry passage (20) of the housing (16), in which passage envelope a collection channel (64) extends at least partially.

7. The furnace as claimed in one of claims 1 to 4, characterized in that the process chamber housing (24) is designed as a muffle (26).

8. The furnace according to any of the claims from 1 to 4, characterised in that the suction channel (60) and/or the collection channel (64) are made of graphite or lined with graphite.

9. The furnace according to claim 1, characterized in that it is used for carbonization and/or graphitization of materials.

10. The furnace according to claim 1, characterized in that the material is a fiber (12).

11. The oven according to claim 10, characterized in that the fibers are fibers (14) formed of oxidized polyacrylonitrile PAN.

12. The furnace according to claim 2, characterized in that in operation of the furnace (10) there is a temperature in said zone lower than 900 ℃.

13. The furnace according to claim 2, characterized in that in operation of the furnace (10) there is a temperature in said zone lower than 800 ℃.

14. The furnace according to claim 7, characterized in that the muffle (26) is made of graphite.